SU144157A1 - Method for distilling off hydrogen chloride from hydrochloric acid - Google Patents
Method for distilling off hydrogen chloride from hydrochloric acidInfo
- Publication number
- SU144157A1 SU144157A1 SU691513A SU691513A SU144157A1 SU 144157 A1 SU144157 A1 SU 144157A1 SU 691513 A SU691513 A SU 691513A SU 691513 A SU691513 A SU 691513A SU 144157 A1 SU144157 A1 SU 144157A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- hydrochloric acid
- hydrogen chloride
- distilling
- reflux
- reflux condenser
- Prior art date
Links
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
По известным способам отгонка хлористого водорода из ооллмой кислоты осуществл етс либо по принципу простой отгочки, либо гутем применени дефлегматора дл образовани флегмы, которую затем возвращают в ректификационную колонну.According to known methods, the removal of hydrogen chloride from oolmoic acid is carried out either by the principle of simple otgochki or by using a reflux condenser to form a phlegm, which is then returned to the distillation column.
Последний способ, как и первый, не дает надлежащего эффекта, так как образующа с флегма составл ет ограниченное количество примерно 20% от веса выдел емого хлористого водорода. К тому же малый объем флегмы требует тарельчатой конструкции укрепл ю хей части колонны и обуславливает низкий коэффициент теплопередачи в теплообменнике-дефлегматоре.The latter method, like the first, does not give the proper effect, since the reflux produced is a limited amount of about 20% by weight of the emitted hydrogen chloride. In addition, a small amount of reflux requires a plate-like structure that strengthens the core of the column and causes a low heat transfer coefficient in the heat exchanger-dephlegmator.
Предлагаемый способ лишен указанных недостатков и состоит в том, что роль флегмоной жидкости играет часть исходной сол ной кислот, специально задаваемой в дефлегматор-абсорбер.The proposed method is devoid of the indicated disadvantages and consists in the fact that the role of cellulitis fluid is played by a part of the initial hydrochloric acid, which is specially specified in the reflux condenser-absorber.
Исходна сол на кислота насыщаетс в дефлегматоре-абсорбере хлористым водородом и на выходе из него имеет тот состав, что и естественна флегмова жидкость. При флегмовом числе 1,2 (за счет искусственной флегмы, близкой к 1) достигаетс наиболее выгодное использование расходуемого холода и тепла, а также теплообменной i:oверхности .The initial hydrochloric acid is saturated in the reflux condenser with hydrogen chloride and at the outlet of it has the same composition as the natural reflux liquid. With a reflux ratio of 1.2 (due to artificial reflux close to 1), the most advantageous use of the consumed cold and heat, as well as heat exchange i: o the top, is achieved.
Отличительна особенность иредлагаемого способа состоит в том, что процесс отгонки ведут с применение.м искусственной флегмы, которую создают укреплением части исходной сол ной кислоты в дефлегматоре-абсорбере .A distinctive feature of the proposed method is that the distillation process is carried out with the use of artificial phlegm, which is created by strengthening part of the initial hydrochloric acid in the reflux condenser-absorber.
Пример. Осуществление процесса по сн етс схс.ой. Псходна 32%-на сол на кислота раздел етс на 2 потока: поток а- 310 кг/час; поток б-50 кг/час. Пот .ж а подогреваетс в кип тильнике от 65 до 80° и далее поступает на тарелку питани ректификационной колонExample. The implementation of the process is explained in cc. The initial 32% hydrochloric acid is divided into 2 streams: a stream a - 310 kg / h; flow b-50 kg / hour. The pot is heated in a boiler from 65 to 80 ° and then fed to the food plate of the distillation column.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU691513A SU144157A1 (en) | 1960-12-30 | 1960-12-30 | Method for distilling off hydrogen chloride from hydrochloric acid |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU691513A SU144157A1 (en) | 1960-12-30 | 1960-12-30 | Method for distilling off hydrogen chloride from hydrochloric acid |
Publications (1)
Publication Number | Publication Date |
---|---|
SU144157A1 true SU144157A1 (en) | 1961-11-30 |
Family
ID=48299859
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SU691513A SU144157A1 (en) | 1960-12-30 | 1960-12-30 | Method for distilling off hydrogen chloride from hydrochloric acid |
Country Status (1)
Country | Link |
---|---|
SU (1) | SU144157A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1052732C (en) * | 1990-10-26 | 2000-05-24 | 辽宁省肿瘤研究所 | Natural anti-cancer leukonuclein made from animal spleens |
-
1960
- 1960-12-30 SU SU691513A patent/SU144157A1/en active
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1052732C (en) * | 1990-10-26 | 2000-05-24 | 辽宁省肿瘤研究所 | Natural anti-cancer leukonuclein made from animal spleens |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
SU144157A1 (en) | Method for distilling off hydrogen chloride from hydrochloric acid | |
JPS56113717A (en) | Distillation device for alcohol | |
JPS56100736A (en) | Purifying method of monochloroacetic acid | |
JPS5525460A (en) | Preparation of red dye | |
SU61737A1 (en) | Method for continuous production of ethyl bromide | |
GB292951A (en) | Improvement in process for the high concentration of nitric acid | |
JPS5592684A (en) | Simple distillation for preparation of low-class distilled spirits | |
JPS5395903A (en) | Stabilization of lower aliphatic fluorochlorohydrocarbons | |
SU99136A1 (en) | Isopropyl alcohol dehydration method | |
JPS5456077A (en) | Reducing method for nonvolatile impurities contained in liquid during evaporation | |
JPS5456076A (en) | Reducing method for nonvolatile impurities contained in liquid during evaporation | |
JPS52125467A (en) | Vertical multi-effect evaporator | |
GB524478A (en) | Improvements in and relating to distilling and rectifying apparatus | |
JPS55122731A (en) | Purification of p-vanillin | |
JPS56147739A (en) | Purification of methylal | |
SU477726A1 (en) | Rectification method | |
JPS5687580A (en) | Separation of trioxane | |
SU64478A1 (en) | The method of regeneration of ammonia from the mother liquors of ammonia-soda production | |
US3474005A (en) | Process for purification of dimethyl sulfide | |
JPS57170976A (en) | Nematic liquid crystal composition | |
GB679179A (en) | Improvements in or relating to the distillation of ethyl alcohol | |
UA11939A1 (en) | Method of wort distillation | |
GB826219A (en) | Stabilization of aqueous colloidal solutions of silica | |
JPS5699794A (en) | Production of alcohol | |
GB534374A (en) | Process and apparatus for the dehydration of alcoholic solutions |